Method for producing alkylglycidyl ether
A technology of glycidyl ether and a manufacturing method, which is applied in chemical instruments and methods, electrolysis process, organic chemistry and other directions, can solve the problems of by-produced metal salts, a large amount of water resources, etc., so as to reduce the generation of waste water and effectively utilize water resources. Effect
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Embodiment 1
[0116] To 60.0 g of the composition (A1), 12.0 g of sodium chloride and 528.0 g of ion-exchanged water were added to obtain a chlorohydrin ether-containing composition (A) (containing 42.6 g of chlorohydrin ether).
[0117] Step 1: 10 sheets of anion exchange membranes (AHA manufactured by ASTOM Corporation, effective area 55 cm) 2 ), 11 bipolar membranes (BP-1E manufactured by ASTOM Corporation, effective area 55cm 2 )according to figure 2 Composition (A) containing chlorohydrin ethers in zone 1 of the alternately arranged electrodialysis apparatus (Model EX3B manufactured by ASTOM Corporation), or in zone 2, will consist of 10.0 g of sodium chloride and 490.0 g of ion exchanged The electrolyte aqueous solution composed of water was circulated with a pump under stirring, and the voltage between the cathode and the anode was kept constant at 30V, while a direct current was applied, and the electrodialysis reaction was carried out for 2 hours. The cumulative current flowing ...
Embodiment 2
[0121] In addition to adding 12.0 g of sodium chloride and 438.0 g of ion-exchanged water to 150.0 g of composition (A1) to obtain a chlorohydrin ether-containing composition (A) (containing 106.5 g of chlorohydrin ether), and in step 1, The composition (A) containing the chlorohydrin ether was circulated in the area 1 of the electrodialysis apparatus with a pump under stirring, and the electrodialysis reaction was carried out in the same manner as in Example 1 for 2 hours. The cumulative current flowing is 12.0Ah, and the average current density is 1000A / m 2 , the liquid temperature in zone 1 is in the range of 15 to 40 °C.
[0122] After the reaction, 332.8 g of composition (B) were obtained in zone 1 . Component analysis of the composition (B) by gas chromatography revealed that 49.7 g of the chlorohydrin ether of the chlorohydrin ether-containing composition (A) was converted to 2-ethylhexyl glycidyl ether without using an alkali agent. Conversion reactions can be carrie...
Embodiment 3
[0125] In addition to adding 12.0 g of sodium chloride and 378.0 g of ion-exchanged water to 210.0 g of composition (A1) to obtain a chlorohydrin ether-containing composition (A) (containing 149.1 g of chlorohydrin ether), and in step 1, The composition (A) containing the chlorohydrin ether was circulated in the area 1 of the electrodialysis apparatus with a pump under stirring, and the electrodialysis reaction was carried out in the same manner as in Example 1 for 2 hours. The cumulative current of the pass is 12.0Ah, and the average current density is 1000A / m 2 , the liquid temperature in zone 1 is in the range of 15 to 40 °C.
[0126] After the reaction, 319.8 g of composition (B) were obtained in zone 1 . Component analysis of the composition (B) by gas chromatography revealed that 54.8 g of the chlorohydrin ether of the chlorohydrin ether-containing composition (A) was converted to 2-ethylhexyl glycidyl ether without using an alkali agent. Conversion reactions can be ca...
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